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High temperature hydropyrolysis of carbonaceous materials

a carbonaceous material, high temperature technology, applied in the direction of hydrocarbon oil cracking, physical/chemical process catalysts, chemistry apparatuses and processes, etc., to achieve the effect of significant carbon emission reduction and effectively utilized

Inactive Publication Date: 2010-12-23
EXXON RES & ENG CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0008]The heat from a nuclear reactor is applied by the use of a heat transfer medium and heat exchange device transferring the heat from the or nuclear reactor to the process unit in which the process is being operated or to the power cells used for producing electricity. Nuclear heat sources have the capability to generate very high temperatures potentially in excess of 1500° C. and heat of this quality can be used very effectively to provide process heat to the hydropyrolysis and to the other specified uses the primary coolant for the nuclear reactor may be utilized directly provided that it does not become radioactive while in the reactor core. Alternatively, the reactor primary coolant can be passed to a heat exchanger to heat coolant in a secondary coolant loop which can then be used to transfer the heat to the hydropyrolysis unit or the power cells. High temperature heat transfer can be effected using transfer media such as liquids, gases, molten salts or molten metals although molten salts and molten metals will often be preferred for their ability to operate at very high temperatures for high energy densities without phase changes; in addition, corrosion problems can be minimized by appropriate choice of medium relative to the metallurgy of the relevant units.
[0011]Nuclear thermal energy sources are zero carbon emission sources and by using them, hydrocarbon resource utilization for process heat is eliminated along with carbon dioxide evolution associated with burning of the hydrocarbon resource to generate process heat. For perspective, each liter of petroleum resid requires approximately 140 liters of natural gas (methane at 15.5° C.) to heat it to 540° C. and hold it at that temperature for six seconds and, as noted above, about 20 to 25 percent of the crude oil input to a refinery is used in processing. The substitution of zero carbon emission sources therefore offers the potential for significant carbon emission reductions in refinery operations where external process hear can be applied and effectively utilized.

Problems solved by technology

Second, the heat is used to generate hydrogen by a high temperature process such as high temperature steam electrolysis, the sulfur-iodine cycle, the zinc-zinc oxide cycle or even, more conventionally, by steam cracking.

Method used

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  • High temperature hydropyrolysis of carbonaceous materials
  • High temperature hydropyrolysis of carbonaceous materials
  • High temperature hydropyrolysis of carbonaceous materials

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Embodiment Construction

[0015]In FIG. 1, an illustrative hydropyrolysis unit with heat supplied from nuclear reactor as an external thermal source is shown. A nuclear reactor 10 providing thermal energy is used to provide heat by way of a heat transfer medium in line 11 to a steam generator 12 which feeds an electrical generator 13 with steam via line 14. Units A, B C and D are hydrogen generators of different types, of which one will be selected for the unit, all being shown here to show the different utility connections required for each type of generator. Unit A is either a zinc-zinc oxide cycle generator or a sulfur-iodine cycle generator, electricity as required by way of line 16 and heat service through line 17 with a suitable heat transfer medium in line 17 bringing heat from heat transfer line 11. Unit B is a high temperature steam electrolysis unit which is supplied with both electricity and steam by way of service lines 16 and 17 respectively. Steam may be taken from steam generator 12 by way of ...

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Abstract

Heat from nuclear reactor as a source of thermal energy is applied to the conversion of carbonaceous materials such as heavy petroleum crude oils, coals and biomass to liquid hydrocarbons. The heat is applied to provide at least a portion of the process heat used in the high temperature, short contact time hydropyrolysis of the carbonaceous material which is supplied with hydrogen generated by a high temperature process such as high temperature steam electrolysis, the sulfur-iodine cycle, the hybrid sulfur cycle, the zinc-zinc oxide cycle, a solid oxide fuel cell or by methane steam cracking. The heat from the nuclear reactor may be used to generate electricity to operate high temperature steam electrolysis used in generation of the hydrogen. By the use of nuclear thermal energy, hydrocarbon resource utilization for process heat is eliminated along with carbon dioxide evolution associated with burning of the hydrocarbon resource to generate process heat. The substitution of zero carbon emission sources therefore offers the potential for significant carbon emission reductions in refinery operations where external process heat can be applied and effectively utilized.

Description

CROSS REFERENCE TO RELATED APPLICATIONS[0001]This application claims priority under 35 USC 120 from Application Ser. No. 61 / 268,776, filed 16 Jun. 2009. It is also related to Application Ser. No. 60 / 268,779, of even date, which relates to the pyrolysis of carbonaceous materials at high temperatures using external process heat from a solar thermal energy source.FIELD OF THE INVENTION[0002]This invention relates to the pyrolysis of carbonaceous materials and more particularly to the hydropyrolysis of carbonaceous materials at high temperatures using external process heat from a nuclear heat source.BACKGROUND OF THE INVENTION[0003]The petroleum refinery is one of the most thoroughly integrated operations in existence: apart from contaminants, all that goes into the refinery is either consumed in processing or emerges as useful product. Increasing shortages of crude oil and their accompanying price increases together with the unpredictable instabilities of many crude-producing regions h...

Claims

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Application Information

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IPC IPC(8): C10B53/06C10B53/00C10G1/00
CPCC10G1/06C10G47/22
Inventor SISKIN, MICHAELVARADARAJ, RAMESHWEISSMAN, WALTERGREANEY, MARK A.
Owner EXXON RES & ENG CO
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